Resilient biodegradable packaging materials

ABSTRACT

Biodegradable starch-based extruded products and methods of manufacturing those products are provided. In particular, extruded starch products processed by compression, stretching or compression and stretching provide excellent flexibility, pliability, dimensional stability, resiliency, abrasion resistance and other properties making them attractive for use as packaging materials.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No.10/000,590, filed Oct. 25, 2001, now U.S. Pat. No. 6,805,823 which is acontinuation of U.S. patent application Ser. No. 08/784,859, filed Jan.15, 1997, now abandoned, which is a continuation-in-part of U.S. patentapplication Ser. No. 08/421,720, filed Apr. 14, 1995, issued as U.S.Pat. No. 5,766,529, all of which are incorporated in their entirety byreference herein.

FIELD OF THE INVENTION

This invention relates generally to expanded biodegradablestarch-containing products with improved flexibility, pliability orresiliency and other properties appropriate for use as packagingmaterials, particularly for extruded sheets, molded trays and otherpackaging containers. The invention includes improved methods formanufacture of expanded starch products and starch-containing extruderfeed compositions.

BACKGROUND OF THE INVENTION

Biodegradable materials are presently in high demand for applications inpackaging materials. Commonly used polystyrene (“Styrofoam”(Trademark)), polypropylene, polyethylene, and other non-biodegradableplastic-containing packaging materials are considered detrimental to theenvironment. The use of such non-biodegradable materials will decreaseas government restrictions discourage their use in packagingapplications. Biodegradable materials that are flexible, pliable andnon-brittle are needed in a variety of packaging applications,particularly for the manufacture of shaped biodegradable containers forfood packaging.

For such applications, the biodegradable material must have mechanicalproperties that allow it to be formed into and hold the desiredcontainer shape, being resistant to collapse, tearing or breaking. Inaddition, biodegradable materials with resiliency, compressibility andbulk density comparable to, “Styrofoam” (Trademark) “peanuts” are neededin loose-fill packaging applications. Further, biodegradable sheetmaterials having properties comparable to polypropylene and polyethylenematerials are needed, for example, in laminating packaging materials.

Starch is an abundant, inexpensive biodegradable polymer. A variety ofbiodegradable starch-based materials have been proposed for use inpackaging applications. Conventional extrusion of starch producesexpanded products that are brittle, sensitive to water and unsuitablefor preparation of packaging materials. Attempts to prepare starch-basedproducts with flexibility, pliability or resiliency and other mechanicalproperties acceptable for various biodegradable packaging applicationshave generally focused on chemical or physico-chemical modification ofstarch, the use of expensive high amylose starch or mixing starch withsynthetic polymers to achieve the desired properties while retainingbiodegradability. A number of references relate to extrusion, andinjection molding of starch-containing compositions.

U.S. Pat. Nos. 4,133,784, 4,337,181, 4,454,268, 5,322,866, 5,362,778,and 5,384,170 relate to starch-based films that are made by extrusion ofdestructurized or gelatinized starch combined with synthetic polymericmaterials. U.S. Pat. No. 5,322,866 specifically concerns a method ofmanufacture of biodegradable starch-containing blown films that includesa step of extrusion of a mixture of raw unprocessed starch, copolymersincluding polyvinyl alcohol, a nucleating agent and a plasticizer. Theprocess is said to avoid the need for preprocessing of the starch. U.S.Pat. No. 5,409,973 reports biodegradable compositions made by extrusionfrom destructurized starch and an ethylene-vinyl acetate copolymer.

U.S. Pat. No. 5,087,650 relates to injection-molding of mixtures ofgraft polymers and starch to produce partially biodegradable productswith acceptable elasticity and water stability. U.S. Pat. No. 5,258,430relates to the production of biodegradable articles from destructurizedstarch and chemically-modified polymers, including chemically-modifiedpolyvinyl alcohol. The articles made are said to have improvedbiodegradability, but to retain the mechanical properties of articlesmade from the polymer alone. U.S. Pat. No. 5,292,782 relates to extrudedor molded biodegradable articles prepared from mixtures of starch, athermoplastic polymer and certain plasticizers. U.S. Pat. No. 5,403,875relates to blends of starch with acrylic polymers which aremelt-processed into thermoplastic articles. U.S. Pat. No. 5,393,804relates to biodegradable compositions made from starch melts containingconverted starch and plasticizers including polyvinyl alcohol. U.S. Pat.No. 5,095,054 concerns methods of manufacturing shaped articles from amixture of destructurized starch and a polymer.

U.S. Pat. No. 4,125,495 relates to a process for manufacture of meattrays from biodegradable starch compositions. Starch granules arechemically modified, for example with a silicone reagent, blended withpolymer or copolymer and shaped to form a biodegradable shallow tray.

U.S. Pat. No. 4,673,438 relates to extrusion and injection molding ofstarch for the manufacture of capsules. U.S. Pat. No. 5,427,614 alsorelates to a method of injection molding in which a non-modified starchis combined with a lubricant, texturizing agent and a melt-flowaccelerator.

U.S. Pat. Nos. 4,863,655, 5,035,930 and 5,043,196 report expanded starchmaterials in which the starch has at least 45% by weight amylose (highamylose materials). Expanded high amylose starch compositions have alsobeen ‘modified by reaction with oxiranes (e.g. ethylene oxide) andinclude the commercially available “ECO-FOAM” (Trademark) in which thestarch is modified by reaction with propylene oxide. Expanded packagingmaterials made from high amylose starch are too expensive for practicalcommercial use. U.S. Pat. No. 5,314,754 of Knight (May 24, 1994) reportsthe production of shaped articles from high amylose starch.

EP published application EP 712883 (published May 22, 1996) relates tobiodegradable, structured shaped products with good flexibility made byextruding starch having defined large particle size (e.g., 400 to 1500microns). The application, however, only exemplifies the use of highamylose starch and chemically-modified high amylose starch.

U.S. Pat. No. 5,512,090 refers to an extrusion process for manufactureof resilient, low density biodegradable packaging materials, includingloose-fill materials, by extrusion of starch mixtures comprisingpolyvinyl alcohol (PVA) and other ingredients. The patent refers to aminimum amount of about 5% by weight of PVA. U.S. Pat. No. 5,186,990reports a lightweight biodegradable packaging material produced byextrusion of corn grit mixed with a binding agent (guar gum) and water.Corn grit is said to contain among other components starch (76–80%),water (12.5–14%), protein (6.5–8%) and fat (0.5–1%). U.S. Pat. No.5,208,267 reports biodegradable, compressible and resilient starch-basedpackaging fillers with high volumes and low weights. The products areformed by extrusion of a blend of non-modified starch with polyalkyleneglycol or certain derivatives thereof and a bubble-nucleating agent,such as silicon dioxide. U.S. Pat. No. 5,252,271 of Hyrum (Oct. 12,1993) reports a biodegradable closed cell light weight packagingmaterial formed by extrusion of a modified starch. Non-modified starchis reacted in an extruder with certain mild acids in the presence ofwater and a carbonate compound to generate CO₂. Resiliency of theproduct is said to be 60% to 85%, with density less than 0.032 g/cm³.

U.S. Pat. No. 3,137,592 relates to gelatinized starch products usefulfor coating applications produced by intense mechanical working ofstarch/plasticizer mixtures in an extruder. Related coating mixtures arereported in U.S. Pat. No. 5,032,337 to be manufactured by extrusion ofmixture of starch and polyvinyl alcohol. Application of thermomechanicaltreatment in an extruder modifies the solubility properties of theresultant mixture which can then used as a binding agent for coatingpaper.

While significant progress has been made toward non-brittle,starch-based biodegradable packaging materials, there neverthelessremains a significant need for lowering production costs and improvingthe physical and mechanical properties of extruded starch materials.

SUMMARY OF THE INVENTION

The present invention provides methods for producing biodegradableexpanded starch products with improved properties for packagingapplications. These methods comprise the steps of extruding astarch-containing mixture through an expansion die, followed bycompressing the extrudate, for example, by subjecting the extrudate topressure generally perpendicular to the direction of extrusion.Compression can be applied, for example, by use of a rolling device. Theextrusion can be performed using conventional methods and apparatus. Diesize, die shape and/or type of compression used, e.g., rollerconfiguration, are selected to produce a shaped, compressed or rolledextrudate. The compressed or rolled extrudate is optionally subjected tofurther shaping, molding and/or cutting to obtain a desired final shapedarticle to suit the planned application.

It has been found that compressing, or compression combined withstretching of the starch-based extrudate significantly improves theflexibility, pliability,’ mechanical strength and dimensional stabilityof extruded, pressure molded packaging containers. The preferred methodfor compression of the extrudate is by rolling. It has also been foundthat compression or rolling improves the resiliency of extruded, lowdensity expanded starch articles, such as those useful for loose fillapplications. Significant decreases in the brittleness of extrudedstarch products are achieved by compressing, rolling, compressing andstretching or rolling and stretching of the material after extrusion.Application of the methods of this invention allows production ofexpanded starch packaging materials having mechanical propertiessuitable for packaging application using significantly lower levels ofexpensive polymeric plasticizers, e.g., polyols such as polyvinylalcohol.

In the method of this invention, pressure can be applied to the emergingextrudate in a direction generally perpendicular to the direction ofextrusion. Pressure is preferably applied substantially perpendicular tothe direction of extrusion. The pressure applied is preferablysufficient to substantially compress the cells in the extrudate.Surprisingly, it is believed that substantially compressing, orpreferably crushing, the cells of the expanded product significantlyimproves the flexibility, pliability or resiliency of the product andsignificantly reduces brittleness. The preferred method of applyingpressure to the extrudate is rolling the extrudate between opposedrollers. The amount of pressure applied may be varied dependent upon thedesired final properties of the material. Rolling is preferably donewhile the extrudate is still hot, most preferably immediately upon exitof the extrudate from the extruder die.

In another aspect, the present invention provides a method of producingimproved expanded starch products comprising the steps of extruding astarch-containing mixture through an expansion die, followed bystretching the extrudate, for example, by pulling the extrudate in thedirection of extrusion. Stretching can be applied, for example, bypulling the extrudate strand, substantially in the direction ofextrusion, faster than the rate of extrusion. Extrusion can be performedusing conventional methods and apparatus. Die size, die shape and/orstretching rate applied are adjusted to provide desired final propertiesin the extruded product. The stretched extrudate is optionally subjectedto further shaping, molding and/or cutting to obtain a desired finalshaped article to suit the planned application. Stretching of thestarch-based extrudate significantly improves the final properties ofshaped extruded articles, including pressure molded packagingcontainers.

In one embodiment of the method, the extrudate is compresses withoutsubstantial stretching. The preferred way to achieve compression withoutsubstantial stretching is to employ rollers in which roller speed issubstantially matched to the rate of extrusion, so that minimal lateralpressure is applied to stretch the extrudate. In another embodiment ofthe method, the extrudate is stretched, for example by pulling theextrudate strand as it exits the die at rate faster than the extrusionrate. Preferred stretch rates range from about 1.1 to about 1.5.

In yet another embodiment, the extrudate is compressed and stretched.The extrudate can be stretched before, after or at the same it is beingcompressed. Preferably stretching is applied at the same time ascompression. The preferred way to compress and stretch the extrudate isto employ rollers in which the roller speed is set faster than the rateof extrusion. In this case, the extrudate is both rolled and stretched.Roller speeds for stretching are typically set to be less than or equalto 50% faster than the extrusion rate. Preferred roller speeds forstretching are between about 10% to about 20% faster than the extrusionrate. However, the desired amount of stretching is dependent upon thedesired final properties of the product as used herein, a roller speedof 10%, 20%, or 50% faster than the extrusion rate means a 1.1, 1.2 or a1.5 stretch rate of the extrudate, respectively.

The compressed, stretched, compressed and stretched expanded starchproduct is biodegradable and has low brittleness and other propertiesmaking it attractive for use in packaging applications.

In one embodiment, this invention provides improved starch sheets forcushioning and packaging applications. Sheets are preferably prepared byrolling, or rolling and stretching the extrudate, using a flat roller.Rolled expanded starch sheets are generally useful in packaging andwrapping applications and in the manufacture of laminated materials forpackaging applications, such as for manufacture of mailing envelopes andrelated containers. Single-ply, two-ply or multiple ply sheets can beformed by the method of this invention.

In another embodiment, this invention provides improved molded starcharticles, particularly articles that are pressure molded from extrudedcompressed, rolled or rolled and stretched starch sheets. Moldedarticles can have various sizes and shapes including shallow and deeptrays, cups, tubs, tubes and other containers. Molded articles can alsobe single or multiple compartment trays or containers and can also beshaped with internal or external ridges, lips, or rims. The starchextrudate is compressed, rolled, or rolled and stretched prior topressure molding. Pressure molding can employ conventional processes andequipment.

In yet another embodiment, this invention provides improved expandedstarch materials having high resiliency, suitable compressibility, lowdensity, low dusting, and low brittleness for use in loose fillpackaging applications. These improved starch materials are produced bymethods described herein by extrusion, combined with a step ofcompressing or substantially crushing the cells in the extrudate,preferably by rolling the hot extrudate. Loose-fill can be produced in avariety of shapes by choice of suitable combinations of die and rollershapes. This invention provides a loose fill expanded starch productwith resiliency higher than 50% useful for packaging applications.Loose-fill products of this invention have compressibility, flexibilityproperties comparable to “Styrofoam” loose fill.

The methods of this invention can be employed essentially with anystarch composition suitable for extrusion. In particular and preferably,the method can be used with starch compositions in which the majoringredient is raw non-modified starch. The method of this inventionallows the use of significantly lower levels of plasticizers in thestarch extruder feed than previously known to achieve desired mechanicalproperties in the final expanded or molded starch products.

The invention also provides extruder feed mixtures containing raw,non-modified starch for production of expanded starch products whichcontain lower levels of plasticizers, particularly lower levels ofpolymeric plasticizers, such as PVA and related polyols. Extruder feedmixtures of this invention may comprise non-modified starch. To achievelower production costs, extruder feed mixtures preferably contain lessthan 5% (by weight) PVA or related polyhydric plasticizer. Morepreferred extruder feed mixtures contain less than or equal to about2.5% PVA or related polyhydric plasticizer. Most preferred extruder feedmixtures contain no PVA or related polyhydric plasticizer.

It has been found that lighter weight expanded starch articles andexpanded starch pressure molded articles with good mechanical strengthand dimensional stability can be produced by the process of thisinvention from extruder feed mixtures that contain talc.

In another aspect, the invention provides a new extrusion device inwhich a conventional extruder is combined with a pressure device whichcan apply pressure to an extrudate emerging from an extruder diesubstantially perpendicular to the direction of extrusion. The pressureapplied being sufficient to substantially compress or preferably tocrush the cells in the hot extrudate. The amount of pressure applied andthe length of application time of pressure depends upon the desiredfinal properties of the product.

Additional aspects and features of the invention will become apparent inthe following detailed description of the invention.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic drawing of an extrusion/rolling orextrusion/rolling and stretching device useful in practicing the methodsof this invention.

FIG. 2 is a schematic drawing of a flow smoother employed in the deviceof FIG. 1.

DETAILED DESCRIPTION OF THE INVENTION

The process of making shaped extruded starch articles of this inventionis described by reference to the schematic manufacturing extrusionapparatus of FIG. 1. Raw non-modified starch is mixed with desiredadditives, for example in an attached feeder (1), through a feed tube(2) and introduced into the mixing compartment of an extruder (3),preferably a twin screw extruder, for example through an inlet (4). Thefeed tube (2) contains a flow smoother (5). The mixture is further mixedand blended, subjected to shearing, increasing temperature and pressurein the extruder to form a mass which is forced through an expanding die(7). The mass is preferably a homogeneous hot melt. Preferably, the massis plasticized.

As shown in more detail in FIG. 2, the feed tube (2) of the feeder (1)contains a flow smoother (5). This device functions to ensure consistentfeed to the extruder to minimize or prevent surging of feed into theextruder. The device comprises arms or spokes (6) that traverse themouth of the feed tube. Most simply, the device can comprise a set ofcrossed wires secured at and across the mouth of the feed tube. Otherconfigurations of the flow smoother will be readily apparent to those ofordinary skill in the art. It has been found that the quality of theextruded material, particularly the quality of extruded sheets issignificantly improved, if a flow smoother is employed.

The shape of the die determines the shape of the extruded strand and dieshape is typically chosen to prepare a desired shape of expandedproduct. The mixture is typically extruded out of the die at a pressureof about 700 to 2000 psi and the extrudate is at a temperature of about120° C. to about 200° C. at extrusion. The extruder is typically heatedand can have several zones along its length in which temperature isseparately adjustable.

For preparation of pressure molded expanded starch articles, includingtrays, the extrudate is preferably formed as a tube by use of an annularor tubular extruder die. The thickness of the extruded tube ispreferably between about 0.1 and 0.05 inches and more preferably betweenabout 0.1 to 0.03 inches. The extruder tube produced is preferablyimmediately compressed, e.g., by rolling or rolling and stretching,between a pair of flat opposed rollers. Rolling of the tube results in atwo-ply sheet. Multi-ply sheets can be formed by overlaying two or moreextruded tubes followed by compression or rolling. Alternatively, theextruded tube can be split to form a strip which is then compressed orrolled to give a single-ply sheet. The compressed or rolled sheet isoptionally cut, and further shaped. For example, a rolled sheet can bepassed into a pressure mold where it is pressed into the shape of thedesired product. The resulting shaped article can be finished bysmoothing or trimming rough edges or by the application of desiredcoatings. For example, sealants, lubricants, water-resistant orwater-repellant coatings can be applied to achieve a desired surfaceappearance or quality or to minimize loss of water from (or absorptionof excess water by) the shaped article. Dyes, fragrances, preservatives,bactericides may also be included or added into the extrudate used toform a shaped article.

The term sheet is used herein to refer to a generally flat, relativelythin slab of extrudate which is preferably sufficiently thick to allowformation of an expanded starch article which retains dimensionalstability. A sheet as used herein is not intended to include films whichdo not retain dimensional stability. The method of this invention can beemployed to make films, however, sheets are the preferred precursor toshaped extruded molded articles. Preferred sheets for preparation ofextruded starch articles have thickness that is greater than about1/50th of an inch and more preferably greater than about 1/16th of aninch. In general, however, the thickness of the sheet, which isdetermined in part by choice of die and type of compression orstretching applied, e.g., roller gap, is selected to achieve desiredfinal dimensions and properties in the shaped extruded starch article.

It has been found to be beneficial to the quality of the final moldedproduct to pinch the ends of the extruded tube prior to compression orrolling. It is believed that pinching the tube end to form a pillowentraps steam that is beneficial during the compression/rolling processto better maintain the temperature of extrudate on compression/rollingor to provide a humid environment for compression/rolling. Provision ofa steam box at the end of the extruder to enclose the extrudate as it ispassed from the extruder die for compression, e.g., as it is passed tothe roller, will provide similar benefit to the quality of thecompressed or rolled material. It has been found that the length of timebetween rolling and molding has a significant effect on the quality ofthe resultant molded article. Preferably the compressed or rolled sheetis immediately passed to the mold for pressure molding. It is believedthat an important factor in this step is the temperature of the mold inrelation to the temperature of the sheet. The sheet is preferablypressure molded while still hot. Alternatively, the mold itself can beheated to insure consistent quality of product.

Water can be added to the extrusion system during the residence of thebase starch mixture in the extruder to adjust the consistency of thestarch mixture during extrusion and/or to adjust the extent of expansionof the product. Lubricant levels in the extrudate can also be adjustedto improve flow through the extruder. Glycerin levels in the extrudercan also be adjusted to improve flow and/or vary properties of theexpanded product. There is no requirement to remove water from the basemixture in the extruder prior to extrusion. Specifically, there is norequirement to apply subatmospheric pressure to the extrudate orextruded strand to remove water.

Continuing to refer to FIG. 1, the extrudate strand which exits the die(7) is preferably fed through a rolling device (10) having two or morerollers (11) positioned with respect to each other to apply pressure tothe strand substantially perpendicular to the direction of extrusion.Multiple set of rollers can be employed, positioned sequentially alongthe direction of extrusion to sequentially apply pressure to theextrudate. Pressure from each roller employed is preferably appliedsubstantially perpendicular to the direction of extrusion. Each set ofrollers can be set to apply the same or different amounts of pressure tothe extrudate. The rollers in a given set of rollers can form an openingcorresponding to the shape of the desired product. For formation ofexpanded starch sheets, including those which are subsequentlyoptionally pressure molded, one or more pairs of opposed flat rollerscan be employed. Preferably, the rollers exert sufficient pressure uponthe strand to substantially compress the cells, or more preferably crushcells, in the strand. The rollers can also be used to finalize shapingof the expanded product.

The process step of applying pressure to the extrudate strand,preferably by rolling, is an important improvement in the manufacturingprocess of this invention which results in significantly decreasedbrittleness of extruded starch products. The application of pressure asdescribed herein also reduces dustiness and chipping of extrudedproducts and increases bulk density. The roller pressure required toobtain improved properties depends on the shape of the extrudate, cellsize and bulk density of the extrudate which in turn depends on thecomposition of the extrudate including the type of starch and watercontent. The required roller pressure needed to achieve the desiredfinal properties is readily determined for a particular starchcomposition and product shape empirically without the expense of undueexperimentation. In general, roller pressure for making sheet productswill be higher than in making shaped loose fill.

Roller speed can be adjusted to substantially match the extrusion rate.If this is done, minimal stretching of extrudate occurs. Alternatively,the roller speed can be adjusted to be somewhat faster than the rate ofextrusion. In this case, the extrudate is both rolled and stretchedcompression accompanied by stretching, as applied when an extrudate isrolled and stretched, has surprisingly been found to confer improvedproperties on starch articles molded using the compressed and stretchedextrudate. Roller speeds up to about 50% faster than the extrusion speedcan be applied to achieve stretching with compression. Preferred rollerspeeds for stretching and compression are between about 10% to about 20%faster than the rate of extrusion.

The substantially compressed or preferably crushed extrudate is cut intodesired lengths by a cutting device, for example with a rotating knifepositioned after the rollers. For preparation of loose fill, theresultant cut strands are preferably cured under controlled temperatureand humidity conditions. Loose fill curing is preferably done between18°30° C., and more preferably at about 21° C., at humidity ranging fromabout 40%–about 80%, and more preferably at about 50% humidity, forabout 1 or 2 days.

The manufacture of expanded starch loose fill and expanded starch sheetsis typically done in a continuous mode by continuous feed into theextruder, extrusion, compression/rolling and cutting.

A conventional twin screw extruder having feed screws, single leadscrews, shear paddles (preferably 3 or more, 3–10 being typical) andmixing paddles (typically 1–5) can be employed in this process. Anexpanding type screw configuration can be used in the twin-screwextruder. Typical residence time of the base mixture (i.e. the starchwith any additives) in the extruder is from about 9 to about 20 secondsand extrusion occurs at a rate from about 100 to about 200 lb/h per dieinsert.

The size and configuration of the die opening determines thecross-sectional shape of the extrudate strand. A variety of shapes andsizes of final products can be made. The starch can also be extruded asan expanded sheet to make sheets of cushioning material or for furthershaping through pressure molding. Typically, product sheets having athickness of about 1/10 to about ¼ inch can be made by theextrusion/compression method. Extruded starch products for loose fillpackaging material, for example, can have several cross-sectionalshapes, including among others, capital omicron, FIG. 8, short rods,S-shaped, C-shaped, oval, and an omega. The product shape does notsignificantly effect resiliency of loose fill packing material. Bulkdensity of loose fill can, however, be dependent upon shape.

A preferred rolling device applies pressure to the extrudate strandsubstantially perpendicular to the direction of extrusion. The hotextrudate strand can simply be passed through opposed flat rollers(which may distort the shape imposed by the die). Generally, it ispreferred that the roller or rollers apply pressure symmetrically to thehot extrudate conforming to the desired product shape, e.g., a rolledsheet is preferably employed for pressure molding of trays and likecontainers. Rollers can be made of stainless steel, teflon or a relatedmaterials that are inert to the extrudate. Rollers are preferablypositioned with respect to the extruder die such that the hot extrudatestrand can be directly fed into the rollers while the extrudate strandis still hot.

A compression or rolling step has not previously been applied to theproduction of expanded starch products. Preferred rollers arespring-loaded and the pressure applied is adjustable. While rolling isthe preferred method for applying pressure to the extruded strand toachieve desired properties in expanded starch articles, those ofordinary skill in the art will appreciate that other methods may beapplied to achieve the desired result. It will also be appreciated thata variety of methods are available to stretch the extrudate. Inparticular, a variety of methods are available for stretching theextrudate before, during or after compression.

Preferably, rollers are positioned sufficiently close to the extruderdie so that the extrudate remains hot during rolling. For ease ofillustration, the roller device of FIG. 1 shows one set of rollers. Twoor more sets of rollers in sequence can be employed in the processingmethod of this invention. The use of more than one set of rollers mayimprove process efficiency. However, care should be taken to keep theextrudate hot during the process of rolling. Rollers may be heated. Forproduction of starch sheets, in particular, the use of two or morerollers may be preferably to achieve desired final properties.

The shape of loose fill packaging material affects the interlockingcapability of the material. Loose fill shaped so that there is someinterlocking between pieces is less readily displaced by jostling andbetter protects packaged items from impact damage. Loose fill shapespreferred for interlocking capability are those with protrusions orindentations which allow pieces to interlock.

The preferred extruder feed compositions of this invention contain rawnon-modified starch as a major ingredient (about 70% to about 97% byweight). Minor amounts of additives, including lubricant, plasticizer,humectant, nucleating agent and another blowing agent (in addition towater) wherein the additives preferably comprise up to a maximum of 30%by weight of the total weight of the extrudates, may be added. One ofthe preferred extrudates contains a minimum amount of plasticizers,including polyvinyl alcohol or ethylene vinyl alcohol (or other polyols)to obtain desired properties when processed by the improvedextrusion/compression method described herein. In particular, preferredextruder feed contains less than about 5% by weight of polyvinyl alcoholor ethylene vinyl alcohol. More preferred extruder feeds contain lessthan or equal to about 2.5% by weight or contain less than or equal toabout 1% by weight of polyvinyl alcohol or ethylene vinyl alcohol.

Water is typically added to the extruder feed during its passage throughthe extruder, most typically at the inlet portion of the extruded. Addedwater may generally represent about 30% or less of the starchcomposition in the extruder. Additional variable amounts of water arepresent in the starch itself. The amount of water added in a givenextrusion will depend on the extrusion conditions, the initial watercontent of the starch used and the desired product. Generally, theamount of water in the extrudate is adjusted to maximize expansion ofthe extruded product, while avoiding a soft or runny extrudate. Watercan be premixed with or added separately from other base starch mixtureingredients. For example, water can be added, and its addition adjustedand controlled, through inlet ports into the extruder. The amount ofwater that must be added depends on the moisture content of the rawstarch. The total water content of the base starch mixture prior toextrusion is typically between about 6% and about 18%.

It has been found that pressure molded articles having suitableproperties for packaging applications, such as containers and trays, canbe prepared using extruder feed compositions which contain no polymericor polyol plasticizer, e.g., no PVA or EVA.

In preferred embodiments, this invention uses raw, non-modified,non-derivatized starch which is essentially starch as it occurs innature other than having been physically separated from other plantcomponents. The starch is typically a powder (fine or coarse) orgranular. Cornstarch is the preferred starch in this invention, howeverany type of non-modified starch from wheat, rice, potatoes, tapioca, orthe like or mixtures of starches can also be used. Mixtures of starchesfrom different plant sources can be employed. In addition, other naturalor synthetic materials that comprise starch as a major component, forexample rice flour, can also be used as the source of starch for theprocess of this invention.

The invention does not require the use of high amylose starch to achievedesired high flexibility or resiliency. The invention does not requirethe use of derivatized starch, such as starch which has been chemicallyreacted at the hydroxy groups (e.g. esterified, etherified orphosphorylated). The invention does not require preconditioning ofstarch by treatment with heat or pressure, gelatinization ordestructurization of starch before addition to the extruder.Nevertheless, starch compositions comprising high amylose starch,modified or derivatized starch or starch compositions that arepreconditioned, gelatinized or destructurized can be processed by theimproved extrusion/compression or and compression and stretching processof this invention to provide extruded materials with improved propertiesfor use as packaging materials. Mixtures of modified or otherwisetreated starch and raw, non-modified starch can be employed the methodsof this invention. Preferred starch for use in this invention ispredominantly non-modified starch, i.e. starch containing 500 or more byweight non-modified starch.

Flexible, pliable or resilient expanded starch products of thisinvention can be prepared with lower levels of in plasticizers,particularly polyvinyl alcohol, ethylene vinyl alcohol and relatedpolyol materials than has been taught in the prior art.

The pre-mixed base starch mixture, the extruder feed (including anyadded water, lubricant, glycerin or other ingredient) can be directlyintroduced into the extruder or the individual components can be addedin any order into the extruder for mixing therein. In a preferred methodof addition of the components, water, lubricant and glycerin are addedto the remaining ingredients in the extruder through independentlyadjustable inlets into the extruder. Extruder feed mixtures of thisinvention predominantly comprise starch with minor amounts of nucleatingagent, such as corn meal or talc.

The preferred extruder feed mixture of this invention predominantlycomprise starch with minor amounts of humectants, plasticizers,lubricants, nucleating agents and optional blowing agents and agentswhich function to reduce cell size. Glycerin, related polyols includingpentaerythritol, and vegetable oil among others may function in starchextrusion as humectants and/or lubricants to improve the flow propertiesof the mixture and provide smooth surfaces for extrusion. Polyvinylalcohol, ethylene vinyl alcohol and related polymeric polyols mayfunction as plasticizers. Glycerin may also function as a plasticizer.Talc, protein as grain meal, in egg albumin or blood meal or otherprotein sources, and materials which generate CO2-like “Hydrocerol”(Trademark, Boehringer Ingelheim) may function as nucleating agents.

Encapsulated sodium bicarbonate and citric acid mixtures for example,Myvaplex, which generates CO, and sodium citrate, for example,“Hydrocerol” (CF and BIH forms, for example, available from BoehringerIngelheim) can act as a nucleating agent. Different forms ofencapsulated material are available in which the encapsulatedingredients are released at different temperatures. Those of ordinaryskill in the art can readily choose the appropriate form for a givenapplication. In general, the form which releases at the lowesttemperature compatible with the application is used. Glycerolmonostearate and other glycerol monoesters of fatty acids may functionto aid in formation of uniform small cells in the extruded material.Superheated water in the extrudate may act as a blowing agent. Theextruder feed of this invention can also include additional minoramounts of blowing agents, including among others carbonate saltsincluding sodium, potassium and ammonium salts. Any vegetable oils orpolyols employed in the base mixture are preferably pumpable. Ingeneral, the extruder feed mixture of this invention may containcombinations of one or more humectants, plasticizers, lubricants,nucleating agents and/or blowing agents. The maximum amount of theseadditives is preferably about 30% by weight of the total weight of theextruder feed mixture (including added water). The extruder feed mixturepreferably contains a minimum of these additives needed to attaindesired properties of extruded product. The base mixture contains aminimum amount of plasticizer to decrease its cost. Thecompression/rolling step of this invention allows the use of much loweramounts of plasticizers than are required in prior art processes toobtain flexible, non-brittle expanded starch products. Preferredextruder feed contain less than about 5% plasticizer. Polymeric vinylalcohols are often employed in starch extrusion processes asplasticizers. The preferred extruder feed mixtures of this inventioncontain less than about 5% by weight of polyvinyl alcohol, polyethylenealcohol or related polymeric vinyl alcohols (or mixtures thereof).Preferred extruder feed mixtures of this invention include those inwhich the amount of polymeric vinyl alcohol is less than about 5% byweight and, specifically, those having less than about 2.5% by weight aswell as those having less than about 1% by weight of polymeric vinylalcohol. PVA having different average molecular weights, is available.Airol 325 and Airol 540, both available from Air Products were foundsuitable in extruder feeds of this invention. Mixtures of this inventionmay also contain relatively low levels of glycerin or other humectants.Mixtures of this invention include those in which glycerin content isless than about 1.5% by weight and those in which glycerin content isless than about 0.5% by weight. Mixtures of this invention also includethose in which talc content is between about 1% by weight to about 10%by weight and those in which talc content is between about 1% by weightand about 5% by weight.

Glycerol monostearate (for example, “Myvaplex” (Trademark, EastmanKodak) can be included in the extruder feed to provide improveduniformity of cell size in the expanded starch. Glycerol monostearate ispreferably included in the extruder feed in an amount ranging from about0.1% to about 0.5% by weight. More preferably, it is present in anamount from about 0.15% to about 0.25% by weight.

For example, extruder feed mixture of this invention can contain thefollowing ingredients expressed in weight percent: starch (about 70% toabout 97%), preferably predominantly raw, unmodified starch; added water(up to about 30%); vegetable oil (up to about 6%); glycerin (up to about3%); polyvinyl alcohol or other plasticizer (up to about 20%, preferredmaximum of less than about 5%); proteinaceous grain meal (up to about20%); glycerol monostearate (up to about 0.5%); additional blowing agent(up to about 0.8%); and talc (up to about 10%) with the provision thatthe mixture must contain a nucleating agent. Additional water and/orlubricant can be added during extrusion.

Other examples of extruder feed mixtures suitable for use in thisinvention include the following where composition is expressed in weightpercent:

Composition A Comprising:

Starch about 60% to about 97%;

Proteinaceous grain meal 0% to about 10%, if present, preferably about4% to about 10%;

Polyvinyl alcohol 0% to about 27%, if present, preferably less thanabout 5%;

Talc 0% to about 20%, if present, preferably about 0.1% to about 10%,more preferably about 0.1% to about 1.5%;

“Myvaplex” (Glycerol monostearate) 0% to about 0.5%, if present,preferably about 0.1% to about 0.3%, more preferably about and 0.2%;

“Hydrocerol” 0% to about 2%, if present, preferably about 0.2% to about0.5%;

with the proviso that a nucleating agent must be present;

Composition B Comprising:

Starch about 70% to about 97%;

Proteinaceous grain meal preferably about 4% to about 10%;

Polyvinyl alcohol 0% or if present, preferably less than about 5%, morepreferably less than about 2.5% or less than about 1%;

Talc 0% or if present preferably about 0.1% to about 1.5%;

“Myvaplex” about 0.2%; and

“Hydrocerol” 0% or is present preferably about 0.2% to about 0.5%;

Composition C Comprising:

Starch about 70% to about 97%;

Proteinaceous grain meal 0% or if present preferably about 4% to about10%;

Polyvinyl alcohol preferably less than about 5%, more preferably lessthan about 2.5% or less than about 1%;

Talc preferably about 0.1% to about 1.5%;

“Myvaplex” about 0.2%; and

“Hydrocerol” preferably about 0.2% to about 0.5%

Composition D Comprising:

Starch about 70% to about 97%;

Proteinaceous grain meal 0% or if present preferably about 4% to about10%;

Polyvinyl alcohol preferably less than about 5%, more preferably lessthan about 2.5% or less than about 1%;

Talc preferably about 0.1% to about 10%;

“Myvaplex” about 0.2%; and

“Hydrocerol” 0%, or if present, preferably about 0.2% to about 0.5%;

Composition E Comprising:

Starch about 70% to about 97%;

Polyvinyl alcohol preferably less than about 5%, more preferably lessthan about 2.5% or less than about

Talc preferably about 0.1% to about 10%; more preferably about 1% toabout 10%;

“Myvaplex” about 0.2%; and

“Hydrocerol” 0%, or if present, preferably about 0.2% to about 0.5%;

Composition F Comprising:

Starch about 70% to about 97%;

Polyvinyl alcohol preferably less than about 5%, more preferably lessthan about 2.5% or less than about 1%;

Talc preferably about 0.1% to about 10%; more preferably about 1% toabout 10%; and

“Myvaplex” about 0.2%;

Composition G Comprising:

Starch about 70% to about 97%;

Talc preferably about 1% to about 10%, more preferably about 5% to about6%; and

“Myvaplex” about 0.2%; and

“Hydrocerol” preferably about 0.2% to about 0.5%;

Composition H Comprising:

Starch about 70% to about 97%;

Polyvinyl alcohol preferably less than about 5%, more preferably lessthan about 2.5% or less than about 1%;

“Myvaplex” about 0.2%; and

“Hydrocerol” preferably about 0.2% to about 0.5%;

Composition I Comprising:

Starch about 60% to about 97%;

Proteinaceous grain meal preferably about 4% to about 10%;

Polyvinyl alcohol up to about 27%;

“Myvaplex” about 0.2%;

Oil, e.g., vegetable oil, 0% to about 1.5%;

Glycerine 0% to about 1.5%; and

“Hydrocerol” preferably about 0.2% to about 1%;

The extruder feed composition of this invention can optionally containcoloring agents, fragrances, bactericides and mould-inhibiting agents.The extruder feed may optionally include various sources of fiber, e.g.,soy fiber. Fiber content can preferably range up to about 10% by weightof the extruder feed, but can be varied to adjust stiffness of extrudedsheets and molded articles.

It has been found that starch materials that have been compressed intosheets and pressure molded may be recycled back into the extrusionprocess by grinding the materials very finely, and combining them withadditional feed composition. For example, it has been found that the useof an extruder feed in which up to about 20% by weight of the starch isground recycled extruded starch results in no significant detriment toproperties of the final extruded, shaped product. Depending upon thedesired final properties of the product, a higher or lower percentage ofrecycled material may be included in the extruder feed for processing.

Resiliency (also called bulk resiliency) is the capability of a materialto recover its size and shape, i.e. to recover its original volume,after deformation by a compressive force. Bulk resiliency of a materialis assessed as percent recovery of volume by measuring the originalvolume (as height of a given amount of material in a container) and thevolume after about a 30-second recovery from the application of acompressive force. The loose fill products made as described herein willgenerally have resiliency of about 50% or more. Preferred loose fillproducts will have resiliency over about 60%, and more preferred loosefill products will have resiliency of about 75% or more. Most preferredloose fill product will have resiliency between about 85% to about 95%.In the present invention, high resiliency is substantially imparted toshaped expanded products by the physical processing step of compression,rolling, or preferably rolling with stretching of the hot extrudedproduct. The minor amounts of humectants and plasticizers that areincluded in the base starch mixture do not in themselves account for thesignificant improvements in resiliency.

Packaging materials can also be compared and assessed based on theirbulk density (weight/unit volume) and bulk compressibility (i.e., themaximum force needed to compress the sample to a preselected % of itsoriginal volume, typically to ⅔ of its original volume). Flexibility,the capability to bend without breaking, can be assessed qualitativelyby applying hand pressure to the final extruded and molded productssqueezing to assess how much force can be applied before the extrudedproduct breaks.

Compressed or rolled extrudates of this invention may have a bulkdensity less than about 2.0 lbs/ft³, but greater than 0.25 lbs/ft³. Thetypical bulk density for corn starch products of this invention is about0.5 to 0.8 lbs/ft³. The material as extruded is typically much lighterthan the final product since the compressing or rolling increases bulkdensity. Expanded starch products have moisture content generally lowerthan the extruder feed material. Typically, the compressed/rolledexpanded products contain from about 5% to about 9% by weight moistureand more typically from about 6% to about 7% by weight moisture.

The mechanical properties of pressure molded and other expanded starcharticle made by the methods of this invention can be evaluated, forexample, by preparation of tensile and Izod bars according to ASTM testmethods, D638-84 and D256-84

The extruded expanded starch products of this invention are useful inapplications of shaped articles for packaging materials. In addition toloose fill packaging material, starch sheets for wrapping or otherapplications can be made by the extrusion/rolling method of thisinvention. In particular, starch sheets produced by methods herein canbe combined with paper and other biodegradable materials to makebiodegradable laminated materials, such as mailing envelopes. Further,articles having a variety of shapes including trays and other containerscan be produced by the methods herein combined with conventional methodsof molding, particularly pressure molding, of expanded starch.

The following examples are illustrative of this invention.

EXAMPLES Example 1 Preparation of Pressure Molded Expanded StarchProducts

Extruded starch sheets useful for pressure molding of trays and othershaped articles with low brittleness, suitable flexibility and usefuldimensional stability were prepared using the extrusion compressionmethod of this invention, exemplified by use of rollers to applycompression to the hot extrudate. Extruder feed compositions useful inthis method include Compositions 1-I detailed above.

The components of the feed mixture were mixed prior to theirintroduction into the extruder. Water was added independently to theextruder. The extruder employed is a Wenger Model TX52 Twin-ScrewExtruder (Wenger Manufacturing, Inc. Sabetha, Kans.) which was adaptedwith feed screws, single lead screw, 5 shear paddles, and 10 mixingpaddles. The extruder barrel has three temperature zones. The mixture isplasticized in the extruder. In general, extruder conditions were set,as is known in the art, to provide smooth flow of extrudate. Moredetails provided below.

Screw Configurations

Standard (#1), high intensity (#2) or medium intensity (#3) screwconfigurations were suitable in extrusions.

Experimental conditions for the extrusion are:

Screw configuration (#1) has the following characteristics:

 4 ea 1.5 D 3/4 Pitch 10 ea Bilobal shear @ 45 deg  4 ea 1.5 D 3/4 Pitch 5 ea Bilobal shear @ 45 deg  1 ea 376 cone screws

Screw configuration (#2) has the following characteristics:

 4 ea 1.5 D 3/4 Pitch 10 ea Bilobal shear @ 45 deg  2 ea 1.5 D 3/4 Pitch 1 ea 1.5 D 1/2 Pitch (cut flight)  1 set Circular shear locks, 6.5 mmthick (36/52 OD)  1 set Circular shear locks, 6.5 mm thick (42/47 OD)  8ea Bilobal shear @ 45 deg  1 set Circular shear locks, 13 mm thick(36/52 OD)  1 ea 387 cone screws

Screw configuration (#3) has the following characteristics:

 4 ea 1.5 D 3/4 Pitch 10 ea Bilobal shear @ 45 deg  2 ea Bilobal shear(thin)  3 ea 1.5 D 3/4 Pitch  1 set Circular shear locks, 6.5 mm thick(42/47 OD)  8 ea Bilobal shear @ 45 deg  1 set Circular shear locks, 6.5mm thick (36/52 OD)  1 set 387 cone screws

Run No. 1

The extruder feed (in weight percent) used was: raw, non-modified cornstarch 92.1%; PVA (Airvol 540) (Air Products) 2.4%); Talc 5.1%;“Myvaplex” 0.2%; and Hydrocerol BIH 0.3%.

Experimental conditions for the extrusion are:

Screw configuration #1, Screw RPM 474 Tube Die (Assembly Dwg 2979025A(BEI) die with adjustable outside die body, die body #2979025A, Mandrel#2979022A. Roller gap 0.203 mm. Roller speed 28 RPM (correspondsapproximately to feed rate to extruder (i.e., extrusion rate). Feed rate63 lb/hr.

Temperatures Z4 180° Z3 100° Z2 70° Z1 120° Water addition 0.21 lbs/minSpecific Mechanical Energy 0.099

The roller speed was set to correspond approximately to the feed rate sothat sheets were rolled, but not stretched. Rolling improved sheetquality and assured more uniform moisture content throughout sheet.Increased flexibility from rolling was apparent. Good quality trays(flexible with dimensional stability) were produced in this run.

Run No. 2

The extruder feed (in weight percent) used was: raw, non-modified cornstarch 94.3%; talc 5.2%; “Myvaplex” 0.2%; and Hydrocerol BIH 0.3%; afeed that contains no PVA. The extruder conditions were:

Screw configuration #1, Screw RPM 500. Same die as in Run 1. Roller gap0.203 mm. Roller speed 17 RPM. Feed rate 63 lb/hr.

Temperatures Z4 180° Z3 100° Z2 700 Z1 136° Water addition 0.25 lbs/minSpecific Mechanical Energy 0.087

Excellent quality trays were made using this method.

Run No. 3

This run employed the same feed as in Run 1 and was intended to evaluatethe use of a higher feed rate and a high intensity screw. The trays madewere excellent quality and no significant difference was observed forvariation of parameters. Extruder conditions:

Screw configuration #2, Screw RPM 480. Same die as in Run 1. Roller gap0.203 mm. Roller speed 17 RPM (sheet stretched and rolled. Feed rate72.8 lb/hr.

Temperatures Z4 180° Z3 1000 Z2 70° Z1 153° Water addition 0.32 lbs/minSpecific Mechanical Energy 0.11

Run No. 4

This run employed recycled extruded sheet (about 10% by weight of thetotal extrudate). The extruder feed (in weight percent) used was: totalstarch 92.1% (raw, non-modified cornstarch plus recycled extruded starchsheet, made using the formula of Run 1 above); PVA 2.4%; talc 5.1%;“Myvaplex” 0.2% and Hydrocerol BIH 0.3%. Recycled extruded sheet is theremains of previous extruder test runs. The materials for recycling werefirst flaked in a flaker and then ground three times to a fineconsistency in a Fitz mill. The ground material was blended with freshmaterial in a ribbon blender; the blend time was standard, about 15 min.The trays made from feed containing recycled extruded sheet were pliableand had a silken feel. Extruder conditions:

Screw configuration #1, Screw RPM 500. Same die as in Run 1. Roller gap0.203 mm. Roller speed 24 RPM. (Increased as feed rate increased). Feedrate 63 lb/hr. (Increasing to 101 lbs/hr.)

Temperatures Z4 180° Z3 100° Z2 70° Z1 127° Water addition 0.25 lbs/minSpecific Mechanical Energy 0.099

Example 2 Preparation of Loose Fill Packaging Material

A high resiliency (about 85% to about 95%) loose-fill packaging materialin the shape of a rod is prepared employing a base mixture having thefollowing components listed as weight %:

weight % unmodified corn starch 77.7 water 2.8 vegetable oil 0.97glycerin 1.6 polyvinyl alcohol 4.9 corn meal 9.7 “Myvaplex” (Trademark,0.39 Eastman Kodak, monoglyceride of stearic acid, i.e glycerolmonostearate) talc 1.9

The corn starch employed had about 22 wt % amylose and about 8% to about15% water by weight. The polyvinyl alcohol used had molecular weightrange 200,000 to 300,000.

These ingredients, except water, vegetable oil and glycerine were mixedprior to introduction into the extruder. Water, vegetable oil andglycerine were added independently to the extruder through separateinlets. The extruder employed was a Wenger Model TX52 Twin-ScrewExtruder (Wenger Manufacturing, Inc. Sabetha, Kans.) which was adaptedwith feed screws, single lead screws, 5 shear paddles, 10 mixing paddlesand a 100 mil diameter die insert to produce a rod shaped extrudate. Theextruder barrel had three temperature zones (150 Z6 [actual temperature144° C.], 90 Z5 [actual temperature 139° C.] and 70 Z4 [actualtemperature not measured]). The screw rpm was 495. The plasticized masswas extruded at a rate of 110 lb/h at 1000 psi and the extrudate was ata temperature of about 175° C. The residence time of the material in theextruder was about 13 seconds.

The extruded material was rolled perpendicular to the direction ofextrusion to substantially compress the cells therein. Subsequent torolling, the stand can be cut into small approximately equal-lengthsegments (about 1 inch in length). The expanded, rolled and cut productswere cured at 21° C. in a 50% humidity for 24 h. The cured product hadexcellent resiliency and abrasion resistance.

Example 3 Laminated “Kraft” (Trademark) Paper for Packaging Applications

A base mixture of this invention is introduced into an extruder, such asthe twin-screw extruder described in Example 1, adapted with a flat orslot die to form extruded sheets. The extruded sheets are rolled byrollers, preferably two sets of flat rollers, exerting pressureperpendicular to the extrusion direction and perpendicular to the planeof the sheet. The pressure exerted on the sheet was sufficient tosubstantially crush the cells in the sheet. The rolled sheet iscollected, if desired, by winding onto a roll and is cut along its widthto form desired sheet lengths. The rolled sheet material is cured atabout room temperature under medium humidity (about 40–60%.).

The resulting pliable starch sheet can be directly employed in packagingapplications or can be used in laminated packaging products. Laminatedpackaging products include, among others, “Kraft” paper laminated withpliable starch sheet.

“Kraft” paper is moistened with water, an appropriately sized starchsheet is positioned over the moistened paper and the layered paper andstarch sheet are rolled to ensure overall contact and adhesion of thetwo layers. Additional layers of paper and or starch sheets can be addedby similar steps to obtain a multi-layer laminated material. “Kraft”paper with a single layer (about 1/10–about ¼ inch thick) of starchsheet can be used to fabricate padded envelopes or other mailingcontainers.

All of the references cited in this specification are incorporated intheir entirety by reference herein.

Those of ordinary skill in the art will appreciate that variants,alternatives, substitutes and equivalents of the devices, methods,techniques, expedients, and ingredients specifically described hereinmay exist and that all such variants, alternatives, substitutes andequivalents that can be employed or readily adapted in the methods andcompositions of this invention are within the spirit and scope of thisinvention which is defined by the appended claims.

1. A continuous method for producing sheets and shaped articles, saidmethod comprising: introducing using a flow smoother an extruder feedcomposition comprising starch into an extruder; extruding saidcomposition through a die to generate a tube extrudate; compressing thetube extrudate to form a sheet; and shaping said sheet to form shapedarticles.
 2. A method according to claim 1, further comprising asteaming step after the extruding step and before the compressing step,wherein the steaming step comprises applying steam to the tube extrudatebefore compressing the extrudate.
 3. A method according to claim 1,further comprising a splitting step after the extruding step and beforethe compressing step, wherein the splitting step comprises splitting thetube extrudate to form a strip before the extrudate is compressed.
 4. Amethod according to claim 1, wherein the compressing step comprisepassing the extrudate between at least one pair of opposed rollers.
 5. Amethod according to claim 1, wherein the compressing and shaping stepscomprise passing the extrudate between at least one pair of opposedrollers to form shaped articles.
 6. A method according to claim 1,further comprising stretching said tube extrudate as it exists the diebefore the compressing step.
 7. A method according to claim 6, whereinsheet is shaped utilizing a mold.
 8. A method according to claim 7,wherein the mold is heated.
 9. A method according to claim 1, whereinthe compressed tube extrudate comprises fibers.
 10. A method accordingto claim 1, wherein up to about 20% by weight of the starch of theextruder feed composition comprises recycled extruded starch.
 11. Amethod according to claim 1, wherein the compressing step furthercomprises combining another material with the extrudate to form abi-layered sheet or article.
 12. A method according to claim 1, whereinthe compressing step further comprises compressing the tube with anotherextrudate.
 13. A method according to claim 1, wherein the compressingstep comprises two or more sets of rollers, and optionally a mold.
 14. Amethod according to claim 1, wherein the compressed extrudate comprisesa bulk density of about 0.25 lbs/ft3 to about 2.0 lbs/ft3.
 15. A methodaccording to claim 1, wherein the extruder feed composition comprisesfibers.
 16. A method according to claim 1, wherein the shaped articleshave a coating applied thereto.
 17. A method according to claim 1,wherein the extrudate includes at least one additive selected from thegroups consisting of dyes, fragrances, preservatives and bactericides.18. A method according to claim 16, wherein the coating is selected fromthe group of coatings consisting of sealants, lubricants,water-resistant and water repellant coatings.
 19. A method according toclaim 1, wherein the extruder feed composition further comprises up toabout 0.5% by weight glycerol monosterate, up to about 10% by weighttalc, up to about 5% by weight vinyl alcohol, up to about 0.5% by weightsodium citrate or sodium bicarbonate and citric acid mixtures, and up toabout 10% by weight proteinaceous grain meal.
 20. A method according toclaim 1, wherein the extruder feed composition further comprisesproteinaceous grain meal up to 10% by weight.
 21. A method according toclaim 1, wherein the extruder feed composition further comprises up toabout 27% by weight polyol.
 22. A method according to claim 1, whereinthe extruder feed composition further comprises talc up to about 20% byweight.
 23. A method according to claim 1, wherein the extruder feedcomposition further comprises glycerol monosterate up to about 0.5% byweight.
 24. A method according to claim 1, wherein the extruder feedcomposition further comprises sodium citrate up to about 2% by weight.25. A method according to claim 1, wherein the extruder feed compositionfurther comprises a mixture of sodium bicarbonate and citric acid up toabout 0.5% by weight.
 26. A method according to claim 1, wherein theextruder feed composition comprises about 70% to about 97% by weightpredominantly non-modified starch.
 27. A method according to claim 1,wherein the extruder feed composition comprises more than one type ofstarch.
 28. A method according to claim 4, wherein the rollers of thecompressing step run faster than an extrusion rate such that the tubeextrudate is stretched prior to the compressing step.
 29. A methodaccording to claim 3, wherein the compressing step comprises passing thetube extrudate between at least one pair of opposed rollers, saidrollers running faster than an extrusion rate such that the split opentube extrudate is stretched prior to the compressing step.
 30. A methodaccording to claim 1, wherein the extruder feed composition comprises upto about 3% by weight glycerin.
 31. A method according to claim 1,wherein the extruder feed composition comprises up to about 6% by weightvegetable oil.
 32. A method according to claim 1, wherein the extruderfeed composition comprises up to 30% by weight added water.